Chemical Properties of Cetene (CAS 629-73-2)

InChI

InChI=1S/C16H32/c1-3-5-7-9-11-13-15-16-14-12-10-8-6-4-2/h3H,1,4-16H2,2H3

InChI Key

GQEZCXVZFLOKMC-UHFFFAOYSA-N

Formula

C16H32

SMILES

C=CCCCCCCCCCCCCCC

Molecular Weight¹

224.43

CAS

629-73-2

Other Names

• 1-Cetene
• 1-hexadecene
• 1-n-Hexadecene
• Hexadec-1-ene
• Hexadecene-1
• Hexadecylene-1
• NSC 60602
• Neodene 16
• n-Hexadec-1-ene
• «alpha»-Hexadecene

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.7210; 0.7213]
ω	0.7213		ChemSep v8.3 pure component data Compiled value
ω	0.7210		KDB
ΔcH°liquid	[-10540.00; -10539.00]	kJ/mol
ΔcH°liquid	-10539.00 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-10540.00 ± 2.00	kJ/mol	NIST
ΔcH°solid	-10546.00 ± 3.10	kJ/mol	NIST
μ	0.51	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[169.64; 171.60]	kJ/mol
ΔfG°	169.64	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	171.60	kJ/mol	KDB
ΔfH°gas	[-249.30; -247.20]	kJ/mol
ΔfH°gas	-248.65	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-248.00	kJ/mol	KDB
ΔfH°gas	-248.40 ± 2.50	kJ/mol	NIST
ΔfH°gas	-247.20 ± 2.60	kJ/mol	NIST
ΔfH°gas	-249.30	kJ/mol	NIST
ΔfH°liquid	[-330.50; -327.30]	kJ/mol
ΔfH°liquid	-330.50 ± 3.00	kJ/mol	NIST
ΔfH°liquid	-327.30 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-329.40 ± 2.10	kJ/mol	NIST
ΔfusH°	35.92	kJ/mol	Joback Calculated Property
ΔvapH°	[80.10; 80.30]	kJ/mol
ΔvapH°	80.25	kJ/mol	NIST
ΔvapH°	80.25 ± 0.42	kJ/mol	NIST
ΔvapH°	80.30 ± 0.40	kJ/mol	NIST
ΔvapH°	80.30 ± 0.40	kJ/mol	NIST
ΔvapH°	80.10	kJ/mol	NIST
ΔvapH°	80.10 ± 0.20	kJ/mol	NIST
IE	9.50	eV	Relay (1.0) Calculated Property
log10WS	-7.22		Relay (1.0) Calculated Property
logPoct/wat	6.264		Crippen Calculated Property
McVol	232.000	ml/mol	McGowan Calculated Property
Pc	[1330.00; 1340.00]	kPa
Pc	1340.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1330.00	kPa	KDB
Ptriple	2.45e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[267.80; 1600.80]
Inp	1588.00		NIST
Inp	1590.00		NIST
Inp	1600.80		NIST
Inp	1586.00		NIST
Inp	1586.80		NIST
Inp	1588.10		NIST
Inp	1584.00		NIST
Inp	1584.00		NIST
Inp	1590.00		NIST
Inp	1593.00		NIST
Inp	1588.00		NIST
Inp	1579.00		NIST
Inp	1587.00		NIST
Inp	1590.00		NIST
Inp	1591.60		NIST
Inp	1591.90		NIST
Inp	1591.70		NIST
Inp	1591.60		NIST
Inp	1592.70		NIST
Inp	1592.00		NIST
Inp	1593.00		NIST
Inp	1587.00		NIST
Inp	1591.70		NIST
Inp	1591.60		NIST
Inp	1592.70		NIST
Inp	1591.60		NIST
Inp	1591.90		NIST
Inp	1590.00		NIST
Inp	1600.00		NIST
Inp	1592.00		NIST
Inp	1593.00		NIST
Inp	1590.00		NIST
Inp	1594.00		NIST
Inp	1590.00		NIST
Inp	1592.00		NIST
Inp	1593.20		NIST
Inp	1590.00		NIST
Inp	1590.00		NIST
Inp	1588.00		NIST
Inp	1590.00		NIST
Inp	1590.00		NIST
Inp	1595.00		NIST
Inp	1600.00		NIST
Inp	1588.00		NIST
Inp	1586.00		NIST
Inp	1593.00		NIST
Inp	1590.00		NIST
Inp	1589.00		NIST
Inp	1597.00		NIST
Inp	1593.00		NIST
Inp	1581.00		NIST
Inp	1590.00		NIST
Inp	1593.00		NIST
Inp	1590.00		NIST
Inp	1593.00		NIST
Inp	Outlier 267.80		NIST
Inp	Outlier 270.30		NIST
Inp	Outlier 267.80		NIST
Inp	1590.00		NIST
Inp	1588.00		NIST
Inp	1588.10		NIST
I	[1625.70; 1666.00]
I	1666.00		NIST
I	1655.00		NIST
I	1626.00		NIST
I	1625.70		NIST
I	1630.00		NIST
I	1645.00		NIST
I	1647.00		NIST
I	1649.00		NIST
I	1655.00		NIST
I	1644.00		NIST
I	1645.00		NIST
I	1654.00		NIST
I	1654.00		NIST
S°liquid	[587.90; 613.88]	J/mol×K
S°liquid	613.88	J/mol×K	NIST
S°liquid	587.90	J/mol×K	NIST
Tboil	[547.00; 558.02]	K
Tboil	558.02	K	ChemSep v8.3 pure component data Compiled value
Tboil	558.00	K	KDB
Tboil	547.20	K	NIST
Tboil	547.00	K	NIST
Tboil	557.60	K	NIST
Tc	[717.00; 717.04]	K
Tc	717.04	K	ChemSep v8.3 pure component data Compiled value
Tc	717.00	K	KDB
Tfus	[277.15; 291.00]	K
Tfus	277.27	K	ChemSep v8.3 pure component data Compiled value
Tfus	277.30	K	KDB
Tfus	277.23 ± 0.04	K	NIST
Tfus	277.25 ± 0.03	K	NIST
Tfus	277.27 ± 0.02	K	NIST
Tfus	277.25 ± 0.04	K	NIST
Tfus	277.27 ± 0.02	K	NIST
Tfus	277.30 ± 2.00	K	NIST
Tfus	277.15 ± 2.00	K	NIST
Tfus	277.21 ± 0.30	K	NIST
Tfus	277.20 ± 1.00	K	NIST
Tfus	Outlier 291.00 ± 1.00	K	NIST
Ttriple	[277.30; 277.51]	K
Ttriple	277.51	K	ChemSep v8.3 pure component data Compiled value
Ttriple	277.39 ± 0.00	K	NIST
Ttriple	277.51 ± 0.05	K	NIST
Ttriple	277.30 ± 0.15	K	NIST
Ttriple	277.45 ± 0.05	K	NIST
Ttriple	277.39 ± 0.00	K	NIST
Ttriple	277.51 ± 0.05	K	NIST
UQi	9.04		ChemSep v8.3 pure component data Compiled value
URi	11.01		ChemSep v8.3 pure component data Compiled value
Vc	[0.912; 1.008]	m3/kmol
Vc	1.008	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.912	m3/kmol	KDB
Zc	[0.2035770; 0.2490000]
Zc	0.2490000		ChemSep v8.3 pure component data Compiled value
Zc	0.2035770		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[485.83; 488.88]	J/mol×K	[298.15; 298.15]
Cp,liquid	485.83	J/mol×K	298.15	NIST
Cp,liquid	488.88	J/mol×K	298.15	NIST
Csat	[477.10; 549.10]	J/mol×K	[280.00; 380.00]
Csat	477.10	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	481.60	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	485.90	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	487.00	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	493.20	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	500.10	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	507.50	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	515.40	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	523.60	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	532.00	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	540.50	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	549.10	J/mol×K	380.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	[3.87; 30.21]	kJ/mol	[249.20; 277.51]
ΔfusH	3.87	kJ/mol	249.20	NIST
ΔfusH	30.21	kJ/mol	277.50	NIST
ΔfusH	30.21	kJ/mol	277.50	NIST
ΔfusH	30.21	kJ/mol	277.50	NIST
ΔfusH	30.19	kJ/mol	277.51	NIST
ΔfusH	30.19	kJ/mol	277.51	NIST
ΔvapH	[50.42; 61.50]	kJ/mol	[509.50; 558.00]
ΔvapH	61.50	kJ/mol	509.50	NIST
ΔvapH	50.42	kJ/mol	558.00	KDB
ρl	788.00	kg/m3	283.00	KDB
ΔfusS	[15.53; 108.86]	J/mol×K	[249.20; 277.51]
ΔfusS	15.53	J/mol×K	249.20	NIST
ΔfusS	108.86	J/mol×K	277.50	NIST
ΔfusS	108.80	J/mol×K	277.51	NIST
ΔfusS	108.80	J/mol×K	277.51	NIST
γ	0.03	N/m	298.20	KDB

Datasets

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	303.15	1314.4
100.00	313.15	1278.1
100.00	323.15	1242.5
100.00	333.15	1207.6
100.00	343.15	1173.2
100.00	353.15	1139.5
100.00	363.15	1106.4
100.00	373.15	1073.8
100.00	383.15	1041.7
100.00	393.15	1010.2
100.00	403.15	979.2
100.00	413.15	948.7
100.00	423.15	918.8
100.00	433.15	889.2
2500.00	303.15	1327.9
2500.00	313.15	1292.1
2500.00	323.15	1257.1
2500.00	333.15	1222.7
2500.00	343.15	1188.9
2500.00	353.15	1155.8
2500.00	363.15	1123.3
2500.00	373.15	1091.4
2500.00	383.15	1060.1
2500.00	393.15	1029.3
2500.00	403.15	999.1
2500.00	413.15	969.4
2500.00	423.15	940.3
2500.00	433.15	911.7
5000.00	303.15	1341.7
5000.00	313.15	1306.4
5000.00	323.15	1271.9
5000.00	333.15	1238.0
5000.00	343.15	1204.9
5000.00	353.15	1172.3
5000.00	363.15	1140.5
5000.00	373.15	1109.2
5000.00	383.15	1078.6
5000.00	393.15	1048.5
5000.00	403.15	1019.0
5000.00	413.15	990.1
5000.00	423.15	961.8
5000.00	433.15	934.0
10000.00	303.15	1368.2
10000.00	313.15	1333.9
10000.00	323.15	1300.3
10000.00	333.15	1267.5
10000.00	343.15	1235.4
10000.00	353.15	1204.0
10000.00	363.15	1173.2
10000.00	373.15	1143.1
10000.00	383.15	1113.6
10000.00	393.15	1084.8
10000.00	403.15	1056.6
10000.00	413.15	1029.0
10000.00	423.15	1002.0
10000.00	433.15	975.7
15000.00	303.15	1393.7
15000.00	313.15	1360.2
15000.00	323.15	1327.5
15000.00	333.15	1295.6
15000.00	343.15	1264.4
15000.00	353.15	1233.9
15000.00	363.15	1204.1
15000.00	373.15	1175.0
15000.00	383.15	1146.5
15000.00	393.15	1118.8
15000.00	403.15	1091.6
15000.00	413.15	1065.2
15000.00	423.15	1039.3
15000.00	433.15	1014.1
20000.00	303.15	1418.2
20000.00	313.15	1385.5
20000.00	323.15	1353.6
20000.00	333.15	1322.4
20000.00	343.15	1292.1
20000.00	353.15	1262.4
20000.00	363.15	1233.5
20000.00	373.15	1205.2
20000.00	383.15	1177.7
20000.00	393.15	1150.8
20000.00	403.15	1124.6
20000.00	413.15	1099.0
20000.00	423.15	1074.1
20000.00	433.15	1049.8
30000.00	303.15	1464.6
30000.00	313.15	1433.2
30000.00	323.15	1402.7
30000.00	333.15	1372.9
30000.00	343.15	1343.9
30000.00	353.15	1315.7
30000.00	363.15	1288.2
30000.00	373.15	1261.4
30000.00	383.15	1235.3
30000.00	393.15	1209.9
30000.00	403.15	1185.2
30000.00	413.15	1161.2
30000.00	423.15	1137.8
30000.00	433.15	1115.0
40000.00	303.15	1508.0
40000.00	313.15	1477.8
40000.00	323.15	1448.4
40000.00	333.15	1419.8
40000.00	343.15	1392.0
40000.00	353.15	1364.9
40000.00	363.15	1338.6
40000.00	373.15	1313.0
40000.00	383.15	1288.1
40000.00	393.15	1263.8
40000.00	403.15	1240.3
40000.00	413.15	1217.4
40000.00	423.15	1195.2
40000.00	433.15	1173.6
60000.00	303.15	1587.7
60000.00	313.15	1559.3
60000.00	323.15	1531.8
60000.00	333.15	1505.1
60000.00	343.15	1479.1
60000.00	353.15	1453.9
60000.00	363.15	1429.4
60000.00	373.15	1405.5
60000.00	383.15	1382.4
60000.00	393.15	1360.0
60000.00	403.15	1338.2
60000.00	413.15	1317.0
60000.00	423.15	1296.5
60000.00	433.15	1276.6
80000.00	303.15	1659.7
80000.00	313.15	1632.8
80000.00	323.15	1606.8
80000.00	333.15	1581.5
80000.00	343.15	1556.9
80000.00	353.15	1533.1
80000.00	363.15	1510.0
80000.00	373.15	1487.6
80000.00	383.15	1465.8
80000.00	393.15	1444.6
80000.00	403.15	1424.1
80000.00	413.15	1404.2
80000.00	423.15	1384.9
80000.00	433.15	1366.2
100000.00	303.15	1725.7
100000.00	313.15	1700.0
100000.00	323.15	1675.2
100000.00	333.15	1651.1
100000.00	343.15	1627.7
100000.00	353.15	1605.0
100000.00	363.15	1583.0
100000.00	373.15	1561.6
100000.00	383.15	1540.9
100000.00	393.15	1520.8
100000.00	403.15	1501.3
100000.00	413.15	1482.4
100000.00	423.15	1464.0
100000.00	433.15	1446.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[214.47; 931.48]	J/mol×K	[100.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.11325e+02
Coefficient B			-5.83628e+02
Coefficient C			6.98018e+00
Coefficient D			1.78465e-05
Coefficient E			-1.70655e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	214.47	J/mol×K	100.00	Calculated Property
Cp,gas	321.26	J/mol×K	255.56	Calculated Property
Cp,gas	472.45	J/mol×K	411.11	Calculated Property
Cp,gas	596.96	J/mol×K	566.67	Calculated Property
Cp,gas	692.42	J/mol×K	722.22	Calculated Property
Cp,gas	765.68	J/mol×K	877.78	Calculated Property
Cp,gas	822.63	J/mol×K	1033.33	Calculated Property
Cp,gas	867.47	J/mol×K	1188.89	Calculated Property
Cp,gas	903.08	J/mol×K	1344.44	Calculated Property
Cp,gas	931.48	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[471.55; 820.37]	J/mol×K	[277.51; 680.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.52890e+02
Coefficient B			9.66240e-01
Coefficient C			-9.52030e-04
Coefficient D			1.11520e-06
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.			277.51
Temperature range, max.			680.00
Cp,liquid	471.55	J/mol×K	277.51	Calculated Property
Cp,liquid	502.70	J/mol×K	322.23	Calculated Property
Cp,liquid	534.36	J/mol×K	366.95	Calculated Property
Cp,liquid	567.13	J/mol×K	411.67	Calculated Property
Cp,liquid	601.59	J/mol×K	456.39	Calculated Property
Cp,liquid	638.35	J/mol×K	501.12	Calculated Property
Cp,liquid	678.01	J/mol×K	545.84	Calculated Property
Cp,liquid	721.17	J/mol×K	590.56	Calculated Property
Cp,liquid	768.42	J/mol×K	635.28	Calculated Property
Cp,liquid	820.37	J/mol×K	680.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0048534; 0.0001489]	Pa×s	[273.15; 577.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.19380e+01
Coefficient B			1.80550e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			273.15
Temperature range, max.			577.60
η	0.0048534	Pa×s	273.15	Calculated Property
η	0.0023427	Pa×s	306.98	Calculated Property
η	0.0013067	Pa×s	340.81	Calculated Property
η	0.0008099	Pa×s	374.63	Calculated Property
η	0.0005434	Pa×s	408.46	Calculated Property
η	0.0003875	Pa×s	442.29	Calculated Property
η	0.0002899	Pa×s	476.12	Calculated Property
η	0.0002254	Pa×s	509.94	Calculated Property
η	0.0001809	Pa×s	543.77	Calculated Property
η	0.0001489	Pa×s	577.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[78.36; 0.00]	kJ/mol	[277.51; 717.04]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			9.70290e+01
Coefficient B			4.36570e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			1.00000e-07
Critical temperature, Tc (K)			7.17039e+02
Comment			ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 722 K
Temperature range, min.			277.51
Temperature range, max.			717.04
ΔvapH	78.36	kJ/mol	277.51	Calculated Property
ΔvapH	74.43	kJ/mol	326.35	Calculated Property
ΔvapH	70.22	kJ/mol	375.18	Calculated Property
ΔvapH	65.65	kJ/mol	424.02	Calculated Property
ΔvapH	60.63	kJ/mol	472.86	Calculated Property
ΔvapH	55.00	kJ/mol	521.69	Calculated Property
ΔvapH	48.51	kJ/mol	570.53	Calculated Property
ΔvapH	40.64	kJ/mol	619.37	Calculated Property
ΔvapH	30.03	kJ/mol	668.20	Calculated Property
ΔvapH	0.00	kJ/mol	717.04	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[418.16; 577.53]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.60292e+01
Coefficient B			-5.35198e+03
Coefficient C			-7.81760e+01
Temperature range, min.			418.16
Temperature range, max.			577.53
Pvap	1.33	kPa	418.16	Calculated Property
Pvap	2.91	kPa	435.87	Calculated Property
Pvap	5.89	kPa	453.58	Calculated Property
Pvap	11.19	kPa	471.28	Calculated Property
Pvap	20.12	kPa	488.99	Calculated Property
Pvap	34.46	kPa	506.70	Calculated Property
Pvap	56.57	kPa	524.41	Calculated Property
Pvap	89.41	kPa	542.11	Calculated Property
Pvap	136.64	kPa	559.82	Calculated Property
Pvap	202.63	kPa	577.53	Calculated Property
Pvap	[2.45e-05; 1479.47]	kPa	[277.51; 722.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.05262e+02
Coefficient B			-1.30520e+04
Coefficient C			-1.22380e+01
Coefficient D			4.69870e-18
Coefficient E			6.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			277.51
Temperature range, max.			722.00
Pvap	2.45e-05	kPa	277.51	Calculated Property
Pvap	4.04e-03	kPa	326.90	Calculated Property
Pvap	0.14	kPa	376.29	Calculated Property
Pvap	1.72	kPa	425.67	Calculated Property
Pvap	11.17	kPa	475.06	Calculated Property
Pvap	46.26	kPa	524.45	Calculated Property
Pvap	140.45	kPa	573.84	Calculated Property
Pvap	345.32	kPa	623.22	Calculated Property
Pvap	741.52	kPa	672.61	Calculated Property
Pvap	1479.47	kPa	722.00	Calculated Property
Pvap	[3.67e-05; 1440.75]	kPa	[277.51; 722.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			9.53711e+01
Coefficient B			-1.21084e+04
Coefficient C			-1.10487e+01
Coefficient D			2.67612e-06
Coefficient E			0.00000e+00
Temperature range, min.			277.51
Temperature range, max.			722.00
Pvap	3.67e-05	kPa	277.51	Calculated Property
Pvap	4.74e-03	kPa	326.90	Calculated Property
Pvap	0.14	kPa	376.29	Calculated Property
Pvap	1.69	kPa	425.67	Calculated Property
Pvap	10.90	kPa	475.06	Calculated Property
Pvap	46.00	kPa	524.45	Calculated Property
Pvap	143.54	kPa	573.84	Calculated Property
Pvap	359.53	kPa	623.22	Calculated Property
Pvap	765.13	kPa	672.61	Calculated Property
Pvap	1440.75	kPa	722.00	Calculated Property
Pvap	[6.95; 101.09]	kPa	[461.30; 557.92]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41887e+01
Coefficient B			-4.23172e+03
Coefficient C			-1.15859e+02
Reference			Camin, Forziati, et al., 1954
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			461.30
Temperature range, max.			557.92
Pvap	6.95	kPa	461.30	Calculated Property
Pvap	10.05	kPa	472.04	Calculated Property
Pvap	14.23	kPa	482.77	Calculated Property
Pvap	19.75	kPa	493.51	Calculated Property
Pvap	26.92	kPa	504.24	Calculated Property
Pvap	36.09	kPa	514.98	Calculated Property
Pvap	47.65	kPa	525.71	Calculated Property
Pvap	62.01	kPa	536.45	Calculated Property
Pvap	79.66	kPa	547.18	Calculated Property
Pvap	101.09	kPa	557.92	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[791.99; 221.87]	kg/m3	[277.51; 722.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			5.14428e+01
Coefficient B			2.31860e-01
Coefficient C			7.22000e+02
Coefficient D			2.85710e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			277.51
Temperature range, max.			722.00
ρl	791.99	kg/m3	277.51	Calculated Property
ρl	759.33	kg/m3	326.90	Calculated Property
ρl	725.15	kg/m3	376.29	Calculated Property
ρl	689.08	kg/m3	425.67	Calculated Property
ρl	650.56	kg/m3	475.06	Calculated Property
ρl	608.74	kg/m3	524.45	Calculated Property
ρl	562.14	kg/m3	573.84	Calculated Property
ρl	507.79	kg/m3	623.22	Calculated Property
ρl	437.60	kg/m3	672.61	Calculated Property
ρl	221.87	kg/m3	722.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[277.51; 717.04]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			5.68600e-02
Coefficient B			1.37580e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			1.00000e-07
Critical temperature, Tc (K)			7.17039e+02
Comment			ChemSep eq 106, SurfaceTension, ChemSep Tmax 722 K
Temperature range, min.			277.51
Temperature range, max.			717.04
γ	0.03	N/m	277.51	Calculated Property
γ	0.02	N/m	326.35	Calculated Property
γ	0.02	N/m	375.18	Calculated Property
γ	0.02	N/m	424.02	Calculated Property
γ	0.01	N/m	472.86	Calculated Property
γ	0.01	N/m	521.69	Calculated Property
γ	0.01	N/m	570.53	Calculated Property
γ	0.00	N/m	619.37	Calculated Property
γ	0.00	N/m	668.20	Calculated Property
γ	0.00	N/m	717.04	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.15; 0.09]	W/m×K	[277.51; 558.02]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K
Coefficient A			2.03670e-01
Coefficient B			-2.06890e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidThermalConductivity
Temperature range, min.			277.51
Temperature range, max.			558.02
λ	0.15	W/m×K	277.51	Calculated Property
λ	0.14	W/m×K	308.68	Calculated Property
λ	0.13	W/m×K	339.85	Calculated Property
λ	0.13	W/m×K	371.01	Calculated Property
λ	0.12	W/m×K	402.18	Calculated Property
λ	0.11	W/m×K	433.35	Calculated Property
λ	0.11	W/m×K	464.52	Calculated Property
λ	0.10	W/m×K	495.68	Calculated Property
λ	0.09	W/m×K	526.85	Calculated Property
λ	0.09	W/m×K	558.02	Calculated Property

Similar Compounds

Find more compounds similar to Cetene.

Mixtures

• Cetene + LACTIC ACID, ETHYL ESTER

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• The thermodynamic properties of 1-alkenes in the liquid state: 1-Hexadecene
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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